System, installation and network for recovery of gas trapped by fluid and particulate matter in a gas or oil well

ABSTRACT

A system for recovery of gas trapped by fluid and particulate matter in a gas or oil well includes a device having a body defining a cavity with a cap at its upper end and an opening for entry of fluid at its bottom end, a lower valve for controlling flow of fluid into the cavity and an upper valve for controlling flow of the fluid and suspended solids out of the cavity. The cap has a plurality of lines passing therethrough and into the cavity, which includes a gas line for providing a stream of pressurized gas to push downward on fluid in the cavity in a compression stroke which closes the lower valve and opens the upper valve. The gas line is used to exhaust contained gas from the cavity. An effluent line allows exit of the fluid and suspended solids during the compression stroke. A probe line provides electrical power to a pair of probes for initiating and halting entry of the stream of pressurized gas into the cavity. The plurality of lines extend out from a wellhead, wherein the probe line is connected to a source of electricity, the gas line is connected to a source of pressurized gas and the effluent line is connected to a fluid storage unit.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. patent application Ser. No.15/264,790 filed on Sep. 14, 2016, which claims priority to U.S.Provisional Application Ser. No. 62/219,238, filed on Sep. 16, 2015, theentire disclosures of which is incorporated herein by reference in itsentirety.

FIELD OF THE INVENTION

The invention relates to the field of hydrocarbon production and moreparticularly to production of gas from liquid-loaded gas wellscontaining suspended solids such as sand and/or silt.

BACKGROUND OF THE INVENTION

It is well known that oil and gas wells have a finite lifetime and thatthe production rate of an individual well will decrease gradually untilresource extraction no longer becomes profitable or until regulationsmandate that production from the well must be suspended.

In most cases, as oil and gas wells mature, production volumes decreaseas the bottom-hole pressure decreases. This results in produced fluidsfrom the reservoir reaching a critical velocity that eventually does notpermit the liquids to reach the surface without some form of artificiallift. When these liquids aren't completely removed from the well withthe oil and gas production from the reservoir, they build up in thewell, causing the oil and gas to flow intermittently, loweringproduction and eventually killing the well. This is phenomenon is knownas “liquid-loading.” Liquid loading is particularly problematic forconventional artificial lift equipment when the liquids containsignificant volumes of particulates such as fine mud, sand and silt.

PCT Publication No. WO2010/009496 describes a gas displacement pump foruse in pumping liquids for recovery of oil from stripper wells.

U.S. Pat. No. 5,074,758 describes a pump for moving liquids or slurrieswhich is particularly adapted to move dangerous and corrosive liquids.

U.S. Pat. No. 5,373,897 describes a pneumatic underground fluid recoverydevice for use in a well to pump underground fluids therefrom.

U.S. Pat. No. 6,027,314 describes a pneumatically powered submersiblefluids pump with a casing activator.

There remains a need for a solution to address and improve the rate ofproduction and ultimate reserve recovery from oil and gas wells loadedwith sandy, silty, muddy liquids. In most cases the particulate materialin wells producing these types of liquids in conjunction with oil andgas causes conventional rotating or reciprocating artificial equipmentto fail prematurely. Currently, the problems caused by sand, mud andsilt are addressed using siphon string technology.

SUMMARY OF THE INVENTION

In accordance with one aspect of the invention, there is provided adevice for use in recovery of gas trapped by fluid and suspended solidsin a gas or oil well, the device comprising a body defining a cavitywith a cap at its upper end and an opening for entry of fluid at itsbottom end, the device including a lower valve for controlling flow offluid into the cavity and an upper valve for controlling flow of thefluid and suspended solids out of the cavity, the cap having a pluralityof lines passing therethrough and into the cavity, the lines comprising:a) a gas line for providing a stream of pressurized gas to push downwardon fluid in the cavity in a compression stroke which closes the lowervalve and opens the upper valve, the gas line further used to exhaustcontained gas from the cavity during an exhaust stroke when infiltrationof fluid into the cavity raises the fluid level in the cavity; b) aneffluent line for allowing exit of the fluid and suspended solids duringthe compression stroke; and c) a probe line for providing electricalpower to a pair of probes for initiating and halting entry of the streamof pressurized gas into the cavity.

In certain embodiments, the upper valve and the lower valve are bothlocated below the pair of probes.

In certain embodiments, the probes are spaced vertically apart withinthe cavity in an arrangement having an upper probe for sensing an upperfluid level to trigger initiation of the compression stroke and a lowerprobe for sensing a lower fluid level to trigger initiation of theexhaust stroke.

In certain embodiments, the cavity further contains a plurality ofbaffles for halting upward movement of the suspended solids in the fluidas the fluid rises during the exhaust stroke.

In certain embodiments, each one of the plurality of baffles issupported by one or more of the plurality of lines in the cavity.

In certain embodiments, the plurality of baffles is three baffles.

In certain embodiments, the baffles are leaf-shaped and include openingsfor holding the one or more of the plurality of lines.

In certain embodiments, the leaf-shaped baffles are rotated with respectto each other to provide partial transverse blockage of the cavity atdifferent cross sectional areas of the cavity.

In certain embodiments, one of the openings is configured to hold theeffluent line and another one of the openings is configured to hold theprobe line.

In certain embodiments, the baffles are supported by or formedintegrally with the cavity's sidewall.

In certain embodiments, the effluent line terminates at the upper valveand the upper valve includes an upper ball seat and an upper check ball,wherein the upper valve is closed when the upper check ball ispositioned in the upper ball seat during the exhaust stroke and whereinthe upper valve is open when the upper check ball floats above the upperball seat during the compression stroke.

In certain embodiments, the lower valve is supported by an extension ofthe body which extends below the upper valve and the lower valveincludes a lower ball seat and a lower check ball, wherein the lowervalve is closed when the lower check ball is positioned in the lowerball seat during the compression stroke and wherein the lower valve isopen when the lower check valve floats above the lower ball seat duringthe exhaust stroke.

In certain embodiments, the extension of the body which extends belowthe upper valve is a tube.

Another aspect of the present invention is a device for use in recoveryof gas trapped by fluid and suspended solids in a gas or oil well, thedevice comprising a body defining a cavity with a cap at its upper endand an opening for entry of fluid at its bottom end, the deviceincluding a lower valve for controlling the flow of fluid into thecavity and an upper valve for controlling the flow of fluid out of thecavity, the cap having a plurality of lines passing therethrough andinto the cavity, the lines comprising: a) a gas line for provision of astream of pressurized gas to push downward on fluid in the cavity in acompression stroke which closes the lower valve and open the uppervalve, the gas line further used to exhaust contained gas from thecavity during an exhaust stroke when infiltration of fluid into thecavity raises the fluid level in the cavity; b) an effluent line forallowing exit of fluid suspended solids during the compression stroke;c) a probe line for provision of electrical power to a pair of probesfor initiating or halting the provision of gas pressure to the cavity;and d) a bubble tube line for determining pressure in the device.

In certain embodiments, the bubble tube line is configured to beswitched to a cleaning line for injection of a second stream ofpressurized gas into the device.

In certain embodiments, the device further comprises an adapter attachedto the bottom end of the body, the adapter configured for attachment ofa pair of nested tubes including an inner tube and an outer tube, theadapter having an opening leading to a channel in the adapter's innersidewall, wherein the bottom end of the bubble tube is placed at theopening to transmit gas from the bubble tube into a space between theouter tube's inner sidewall and the inner tube's outer sidewall.

In certain embodiments, the inner tube and the outer tube are attachableto the adapter by threading.

In certain embodiments, the upper valve and the lower valve are bothlocated below the pair of probes.

In certain embodiments, the probes are spaced vertically apart withinthe cavity in an arrangement having an upper probe for sensing an upperfluid level to trigger initiation of the compression stroke and a lowerprobe for sensing a lower fluid level to trigger initiation of theexhaust stroke when the fluid level rises.

In certain embodiments, the cavity further contains a plurality ofbaffles for halting upward movement of the suspended solids in the fluidas the fluid rises during the exhaust stroke.

In certain embodiments, each one of the plurality of baffles issupported by one or more of the plurality of lines in the cavity.

In certain embodiments, the plurality of baffles is three baffles.

In certain embodiments, each of the baffles is leaf-shaped and includesone or more openings for holding the one or more of the plurality oflines.

In certain embodiments, the leaf-shaped baffles are rotated with respectto each other to provide transverse blockage of the cavity at differentcross sectional areas of the cavity.

In certain embodiments, the one or more openings includes a firstopening configured to hold the effluent line, a second openingconfigured to hold the probe line and a third opening configured to holdthe bubble tube line.

In certain embodiments, the baffles are supported by or formedintegrally with the cavity's sidewall.

In certain embodiments, the effluent line terminates below the adapterat the upper valve and the upper valve includes an upper ball seat andan upper check ball, wherein the upper valve is closed when the uppercheck ball is positioned in the upper ball seat during the exhauststroke and wherein the upper valve is open when the upper check ballfloats above the upper ball seat during the compression stroke.

In certain embodiments, the lower valve is supported by the inner tubeof the body which extends below the upper valve and the lower valveincludes a lower ball seat and a lower check ball, wherein the lowervalve is closed when the lower check ball is positioned in the lowerball seat during the compression stroke and wherein the lower valve isopen when the lower check valve floats above the lower ball seat duringthe exhaust stroke.

Another aspect of the present invention is a system for recovery of gastrapped by fluid and particulate matter in a gas or oil well, the systemcomprising: a) a device as described herein wherein the cap is attachedto an upper tube for protecting the plurality of lines extending upwardfrom the cap and the plurality of lines is covered by a singleprotective covering forming an umbilical cable above the cap; and b) awellhead for sealing the well; wherein the plurality of lines extend outfrom the wellhead, wherein the probe line is connected to a source ofelectricity, the gas line is connected to a source of pressurized gasand the effluent line is connected to a fluid storage unit.

In certain embodiments, the wellhead includes a means for gripping theumbilical cable to support the device in the well.

In certain embodiments, the means for gripping the umbilical cable is aset of slips.

In certain embodiments, the wellhead is sealed from the well to preventloss of gas or fluid as a result of potential leakage of the effluentline or the gas line.

In certain embodiments, the system further comprises a means for sealingthe device from the upper tube.

In certain embodiments, the upper end of the protective tube isconnected to a fishing unit for attachment of a lifter for withdrawal ofthe device from the well.

In certain embodiments, the fishing unit comprises a fishing neckattached to a top portion of the protective tube and an overshot tubeconnected to the fishing neck, the overshot tube having a restricteddiameter portion for attachment of the lifter.

In certain embodiments, each one of the plurality of lines is separatedfrom the protective covering within the wellhead and extends from thetop of the wellhead as a separate line.

In certain embodiments, each of the separate lines is each sealed at itsrespective opening at the top of the wellhead.

In certain embodiments, the wellhead includes a production pipeconnected to a gas pipeline and the gas line is connected via athree-way valve to the gas pipeline and a compressor, the three-wayvalve for switching between input of compressed gas into the gas linefor the compression stroke and exhaust of gas back into the pipelineduring the exhaust stroke.

In certain embodiments, each one of the plurality of lines is formed byan upper line and a lower line connected at connection points locatedabove the cap of the separator, the connection points providing a meansfor disconnecting each of the upper lines from their corresponding lowerlines and withdrawing each of the upper lines from the well while thelower lines remain associated with the separator device in the well.

In certain embodiments, at least one of the connection points representsa weak point with respect to disconnection of all of the upper linesfrom their corresponding lower lines.

In certain embodiments, the weak point comprises a connector with alocking spring mechanism having a variable locking set point which, whenexceeded allows breakage of the weak point to allow the upper lines tobe withdrawn from the well.

In certain embodiments, each of the pair of probes is supported withinthe cavity by a connection to the cap.

In certain embodiments, the connection to the cap is made by threadedcap attachments configured to be threaded into the body of the cap withelectrically conducting connector pins extending therethrough forforming a connection of the upper probe line with the pair of probes.

Another aspect of the present invention is a method for removing fluidand suspended solids from a gas or oil well to promote production of gasfrom the well, the method comprising: a) installing a system asdescribed herein in the well; b) injecting the stream of pressurized gasinto the well in the compression stroke to displace liquid into theeffluent line leading out of the well until the level of the fluid andsuspended solids in the well reaches a lower limit indicated by thelower probe; c) halting the pumping of the gas and allowing the liquidto infiltrate into the well in an exhaust stroke until the level of thefluid and suspended solids reaches an upper limit indicated by the upperprobe; and d) repeating steps b) and c) in sequence.

In certain embodiments, the method further comprises collecting dataindicating bottom hole pressure, fluid production volumes and gasproduction volumes to assess the performance of the well.

In certain embodiments, the method further comprises conducting ratetransient analysis from the data, the rate transient analysis providinga means for modelling a rate of gas production decline in the well.

In certain embodiments, step a) is performed by conveying the deviceinto the well using a coiled tubing unit, wherein the coiled tubing unitgrips and drives the umbilical cable as the umbilical cable is conveyedinto the well.

Another aspect of the invention is a wellsite installation forcontrolling production of gas from a gas or oil well, the wellsiteinstallation comprising: a) a system as described herein; b) a controlpanel for controlling and measuring: i) flow of produced gas out of thesystem; ii) flow of the stream of pressurized gas into the system; andiii) flow of the fluid and suspended solids out of the system; and c) aremote terminal unit for collection of data obtained at the controlpanel.

Another aspect of the present invention is a gas collection networkcomprising a plant for receiving and compressing gas produced from aplurality of wellsite installations as described herein, the plantincluding a compressor for compressing the produced gas transferred fromthe wellsite installations and a water tank for storing the fluid andsuspended solids transferred from the well site installations.

In certain embodiments, the plant further comprises a master terminalunit for analysis of the data collected at the control panel.

In certain embodiments, the gas collection network further comprises adehydrator located at the plant to remove water vapor from the producedgas.

In certain embodiments, the gas collection network further comprises amaster terminal unit in data and control communication with the remoteterminal unit, the master terminal unit having a user interfacedisplaying data from the control panel including downhole pressure,casing pressure and flow rate.

In certain embodiments, the gas collection network further comprises afluid line to transmit the fluid and suspended solids to the plant forstorage.

In certain embodiments, the gas collection network further comprises agas recycling line to transmit gas from the dehydrator at the plant tothe wellsite installation as the source of the stream of pressurized gasfor generating the compression stroke.

BRIEF DESCRIPTION OF THE DRAWINGS

Various objects, features and advantages of the invention will beapparent from the following description of particular embodiments of theinvention, as illustrated in the accompanying drawings. The drawings arenot necessarily to scale. Emphasis is instead placed upon illustratingthe principles of various embodiments of the invention. Whereverpossible, similar reference numerals indicate similar components.

FIG. 1 is a schematic cross-sectional view of a system 100 according toone embodiment of the invention.

FIG. 2 is a schematic process diagram indicating how a reservoircomprising oil, water, suspended solids and gas are produced into thewell and moved to a surface pipeline for further processing.

FIG. 3A is a schematic cross sectional view of the separator device 110of the system 100 indicating the flow of gas and fluid during thecompression stroke of the separator device 110 when pressurized gas isinjected into the separator device 110 via the gas line 118.

FIG. 3B is a is a schematic cross sectional view of the device 110 ofthe system 100 indicating the flow of gas and fluid during the exhauststroke of the separator device 110 when pressurized gas is no longerinjected into the separator device 110 and fluid infiltrates from thereservoir into the bottom of the separator device 110.

FIG. 4A is a perspective view of a leaf-shaped baffle 248 a inaccordance with one embodiment of the present invention, which has threeopenings 255 a, 257 a and 259 a for insertion of an effluent line, aprobe line and a bubble tube line, respectively.

FIG. 4B is a perspective view of the same leaf-shaped baffle 248 a shownin FIG. 4A showing protrusion of the effluent line 116, the probe line120 and the bubble tube line 122.

FIG. 5 is a perspective view of the orientation of a set of threebaffles 248 a, 248 b and 248 c showing the effluent line axis 261, theprobe line axis 263 and the bubble tube line axis 265. It is seen thatthe baffles 248 a, 248 b and 248 c are rotated with respect to eachother to provide fluid flow restriction in the cavity of the separatordevice.

FIG. 6A is a perspective view of one embodiment of an adapter 230 forconnection of concentric nesting cylinders to the bottom end of theseparator device to accommodate the bubble tube line.

FIG. 6B is a second perspective view of the adapter embodiment 230 ofFIG. 6A.

FIG. 7 is a perspective view of the adapter embodiment 230 of FIGS. 6Aand 6B shown with the upper ends of the concentric nesting cylinders 132and 134 and the lower end of the separator device body 112 and bubbletube line 122 connected thereto.

FIG. 8 is a cross-sectional view of a bottom portion of one embodimentof the separator device showing detail of the valves residing in theinner cavity 124.

FIG. 9A is a perspective view of a lower wellhead body 269 of apartially assembled wellhead showing the separation of lines from theumbilical cable 162 according to one embodiment of the invention.

FIG. 9B is a perspective view of a partially assembled wellhead with anupper wellhead body 273 attached to the lower wellhead body 269 andshowing the four separate lines 116, 118, 120 and 122 extending from theupper wellhead body 273.

FIG. 9C is a perspective view of an assembled wellhead 268 covered by ahousing 279 and top nut 277.

FIG. 9D is a top view of the housing 279, top nut 277 of the wellhead268 and the four separate lines 116, 118, 120 and 122.

FIG. 9E is a cross sectional view of the wellhead 268 taken across lineL-L of FIG. 9D.

FIG. 10 is a cross section of one embodiment of an umbilical cable 262.

FIG. 11A is a perspective view of one embodiment of a connector systemfor connecting two parts of an effluent line 116 a and 116 b.

FIG. 11B is perspective view of a cross section of the connector systemembodiment of FIG. 12A.

FIG. 11C is a cross sectional view of the same embodiment of FIGS. 12Aand 12B.

FIG. 11D is a magnified view of the circle 12D in FIG. 12C showingdetail of the locking spring 224 and o-rings 227 a and 227 b.

FIG. 12 is a cross section of one embodiment of a pair of probes 301 and311, shown in association with the cap 114 of the separator device.

FIG. 13A is a flow diagram, which is continuous with FIG. 13B, of acontrol system in accordance with one embodiment, showing flow of gas,liquids and data between a separator installation 500 a and a plant 600(FIG. 13B).

FIG. 13B is a schematic flow diagram, continuous with FIG. 13A, of acontrol system in accordance with one embodiment, showing flow of gas,liquids and data between a separator installation 500 a (FIG. 13A) and aplant 600.

FIG. 14 is a plot showing the gas production rate of a gas well in afield test using siphon string technology which is subsequently replacedwith a wellsite installation according to one embodiment of theinvention.

FIG. 15A is a plot of a time course of gas production in a differentfield test in the same wellsite installation described with respect toFIG. 14.

FIG. 15B is a plot of a time course of fluid production in the samefield test referred to in FIG. 15A.

FIG. 15C is a plot of a time course of bubble tube pressure (dashedline) and casing pressure (solid line) in the same field test referredto in FIGS. 15A and 15B.

FIG. 16 is an illustration of a user interface screen showing certainaspects of one embodiment of the control system.

DETAILED DESCRIPTION OF THE INVENTION Rationale

Reservoir pressure depletion resulting from hydrocarbon productioneventually leads to insufficient velocity in the well to allow a gaswell to unload produced fluids. As the fluid level in the verticalwellbore rises, the hydrostatic pressure of the fluid restricts the flowof gas to surface, and production diminishes. Attempts to address thisproblem have typically been prone to early failure or prohibitivelyexpensive, or both. Consequently, liquid-loaded wells are oftenabandoned before all recoverable reserves have been produced.

An additional problem encountered by gas producers in Canada is thatwhen production at a gas well drops below 2 barrels of oil equivalentper day (BOEPD) the operator must post a performance bond with theEnergy Regulator of the particular provincial jurisdiction in accordancewith a regulatory framework known as Licensee Liability RatingLegislature. If gas production falls to zero in a given well, the bondcan be as high as $60,000 per well. If the operator does not post thebond, the Energy Regulator is authorized to shut in the well. Theoperator must then provide $60,000 to abandon the wellbore and thefacilities. With the later issuance of a reclamation certificate, theoperator, upon presentation of the reclamation certificate will bereleased from the bond. This process can take longer than five years insome cases. Including the shut-down costs, a Licensee Management Ratingequal to one can require as much as $120,000 in capital per well with$60,000 required for payment of the bond and $60,000 to actually abandonthe well and reclaim the well site and access road.

It would be advantageous for gas production companies to increase gasproduction and recover more reserves before ultimately being faced witha Limited Liability Rating situation.

About 85 million years ago, a huge inland sea covered the middle ofNorth America. For example, the location of Writing-On-Stone ProvincialPark on the Milk River in southern Alberta, would have been located onthis very large and stormy sea. Sand was deposited on the shore which,over millions and millions of years, slowly compacted to becomesandstone rock. This became part of the Milk River Formation. There area number of regions in this area with high numbers of low-producing gaswells and most of these wells are liquid-loaded.

A well becomes liquid loaded when the fluid velocity in the well fallsbelow 10 feet per second. Dewatering these wells with conventional toolsis problematic due to the nature of the silt and mud in the fluidproduced with the natural gas. A siphon string provides a near-termsolution to this problem because it is constructed of plastic with asmaller inside diameter than most of the shelf steel tubing strings.These plastic strings have a lower coefficient of friction and are lessexpensive when compared to steel strings. However, a more robust andeffective system for recovering gas from liquid-loaded gas and oil wellsis desirable.

Overview and Advantages of the System and Method

The system and method described herein separates gas from liquids inliquid-loaded wells using a separator device provided with downholeprobes to determine when the device is filled with fluid and when it isempty. When the inner cavity of the separator device is full of fluidproduced from the reservoir, an upper probe recognizes the liquid levelat or near the top of the device and triggers the injection of externalpressurized gas in a compression stroke to displace the fluid into aneffluent line where it is pushed out of the well by positive gasdisplacement. The fluid is moved using the pressure of the injected gasand as such does not rely upon reservoir pressure. This fluid in theeffluent line moves directly to a water tank. The silt or othersuspended solids in the fluid may be separated from the fluid and soldas a value-added fertilizer or fill product. The lower level of fluid inthe casing will allow greater volumes of gas to infiltrate into thecasing annulus from the perforations and diffuse upward to the wellheadwhere it is conveyed out of the well and into a pipeline according toconventional processes.

The amount of pressure required to move the fluid into the effluent linedepends on the specific gravity of the fluid and the depth of theseparator device. The fluid produced in the wellbore is moved to thesurface without the benefit of reservoir pressure and minimum velocityrestrictions that cause liquid loading. This fluid is subsequentlyproduced directly to the water disposal tank. Sending fluids directly tothe production tank at a central plant instead of the gas gatheringsystem connected to the plant reduces the pipeline pigging frequency byabout 5-fold and frees up operating personnel to allow them to conductpredictive maintenance at the wells and the plant equipment.

When the fluid is moved out of the separator device via the effluentline, the fluid level drops until a lower threshold is recognized by alower probe. At this threshold, the injection of pressurized gas isstopped and the infiltration of fluid from the well into the separatordevice is allowed to proceed in an exhaust stroke until the fluid levelrises once again (pushing gas out of the cavity of the device via thegas line) to the top probe which once again triggers the injection ofpressurized gas to initiate another compression stroke. The gasexhausted is delivered back to its original source, which, in certainembodiments, is a gas pipeline leading to a processing plant. Arelatively small volume of gas is recycled back to the well to repeatthe cycle. The frequency of cycle depends on the productive capabilityof the reservoir.

One advantage provided by the system and method is that it reduces thefrequency of pigging required to keep the gas-gathering lines fluidfree.

Another advantage is that inflow performance and productivity of awellsite installation with the separator device and system becomesstable and depletion is more predictable extending the recoverablereserve life of a well when the fluid level is constantly below theperforations connecting the reservoir to the wellbore.

Another advantage is that the system is amenable to operation in aninformation network of data analytics, such that a single field operatorcan monitor hundreds of wells online. The operator then only deals withwells that do not meet production expectations. Trouble shooting andrepairs can be done from the computer terminal in most cases. Thisreduces labor costs and time required for maintenance.

Another advantage is that geothermal energy transferred by the fluidsfrom the reservoir to the surface by the system is used to heat theinside of the wellhead shelter. This reduces the need to use methanol toavoid freezing of liquid lines and obviates the need for servicecompanies to thaw frozen lines.

Another advantage is that with operation of the system, the majority offluid and gas separation occurs downhole at the perforations of the welland this minimizes a need for surface separators. This reduces thesurface footprint and reduces the chances of spills which would impactthe environment. Eliminating surface separators reduces property taxes.

Another advantage is that the separator device is deployed in a well byusing a conventional coiled tubing rig with conventional chains and aninjector to grip and lower the umbilical cable containing the linesrequired for operation of the separator device. Furthermore,conventional coiled tubing injection rigs are lighter and are notsubject to seasonal restrictions as are other types of service rigs anddrilling rigs.

Another advantage is that the system containing the bubble tube providesa means for conducting rate transient analysis and as a result,remaining recoverable reserves currently calculated by productiondecline analysis can be verified and calculated using modern ratetransient methods. The optional bubble tube feature of the system whichis described herein below provides a means for continuous measurement ofbottomhole pressures, and continuous producing fluid levels. The datafrom the continuous bottomhole pressure measurement is used to determinethe best drilling spacing to recover unswept reserves in the reservoir.In addition, the bubble tube feature provides a conduit for cleaning ofthe device and the annulus of the well with high pressure gas to breakup larger solid masses that can accumulate in the wellbore whenproducing into the downhole separator.

Another advantage relating to the capability of conducting ratetransient analysis is that new drill spacing units can be determinedbased on pressure draw down analysis to drain unswept reserves. Surfacedrilling footprints based on having fewer wells present helps theenvironment and the economics of developing gas reserves.

Definitions

As used herein, the term “wellhead” refers to the combined components atthe surface of a well that provide the structural andpressure-containing interface for the production equipment. Thefunctions served by the wellhead include, but are not limited to:providing a means for pressure sealing and isolation of the casing atthe surface, providing a means for attachment of equipment such as ablowout preventer, a Christmas tree, a well pump and/or a separatordevice according to the invention, and providing a means for accessingthe well itself, during workover operations for example. A wellhead isalso used to connect the wellhead blowout preventer during workoveroperations using a coiled tubing rig or conventional service rig.

As used herein, the term “umbilical cable” refers to a cable holding thelines which are used to support and operate the separator device of theinvention in a gas well.

As used herein, the term “casing” refers to a pipe inserted into adrilled hole and cemented in place. Casing is installed to protect freshwater formations, isolate a zone of lost returns or isolate formationswith significantly different pressure gradients. Casing is usuallymanufactured from plain carbon steel. After it is installed and cementedin place, it is perforated with holes at various intervals to permitfluids and hydrocarbons under static pressure in the reservoir to beproduced into the wellbore and eventually to the surface.

As used herein, the term “packer” refers to a device for sealing awellbore or a section thereof. A packer will have an initial smallerdiameter which is expandable to seal the wellbore or section thereof.Packers employ flexible, elastomeric elements that expand. The two mostcommon forms are the production or test packer and the inflatablepacker. The expansion of the former may be accomplished by squeezing theelastomeric elements (somewhat doughnut shaped) between two plates,forcing the sides to bulge outward. The expansion of the latter isaccomplished by pumping a fluid into a bladder, in much the same fashionas a balloon, but having more robust construction.

As used herein, the term “weak point” refers to a position along alength of a cable or pipe which is expressly provided as a break pointof the cable or pipe when a pre-determined pulling force is exerted uponthat cable or pipe. A weak point may be provided by alteration of thematerials forming the cable or pipe at the desired position, or may beprovided by an expressly designed mechanical connection structuredesigned to disengage when the pre-determined pulling force is met andexceeded.

As used herein, the term “perforation” refers to a tunnel created in thecasing to the reservoir formation, through which oil or gas enters forproduction.

As used herein, the term “line” refers to any conveyance structure orcombination of connected conveyance structures providing a basicconveyance function over a distance. Accordingly, the related term “gasline” refers to a conduit providing conveyance of gas into and out ofthe separator device of the invention, the related term “effluent line”refers to a conduit for conveying effluent in the form of fluid awayfrom the separator device of the invention, the related term “probeline” refers to an electrical conduit for providing electricity to eachmember of a pair of probes which detect the presence of fluid for thepurpose of controlling compression and exhaust strokes of the separatordevice, and the related term “bubble tube line” refers to a conduit forproviding gas into the separator device for the purpose of pressuremeasurements and for the purpose of cleaning the separator device andthe annulus of the well.

As used herein, the term “compression stroke” refers to the half cycleof the separator device wherein gas is injected into the device to forceliquid and silt out of the cavity of the device via an effluent line.

As used herein, the term “effluent” refers to fluid and suspended solidsdischarged from the separator device according to certain embodiments ofthe invention.

As used herein, the term “exhaust stroke” refers to the half cycle ofthe separator device wherein gas injection is halted and liquids enterthe cavity of the device.

As used herein, the terms “water” and “fluid” are used interchangeablyand refer to water in any mixture state that may be encountered in aliquid-loaded gas well as a result of infiltration from the formationinto the well. The mixture may include oil, dissolved gases, dissolvedmineral salts and suspended solids, including, but not limited to, mud,sand, and silt and precipitated mineral salts.

As used herein, the term “baffle” refers to any structure provided in acavity or channel to block and/or impede the flow of fluids and/orparticulates contained therein.

As used herein, the term “rate transient analysis” refers to analysis ofcontinuous production and flowing pressure data to characterize areservoir for the purposes of determining remaining reserves anddeveloping resource extraction strategy which may be done through infilldrilling or enhanced recovery techniques.

As used herein, the term “fishing” refers to the application of toolsfor removal of objects stuck in a wellbore, which require retrievalusing “fishing tools.”

As used herein, the term “pigging” refers to the act of forcing a devicethrough a pipeline for the purpose of displacing or separating fluidsand for cleaning or inspecting the pipeline. Pigging will reduce backpressure at each wellhead and this will optimize production volumes.

As used herein, the term “bubble tube” refers to a conduit used forinjection of a gas into a well or into equipment installed in a well ata controlled rate for the purpose of continuous measurement of downholepressure. A bubble tube system provides the ability to measure downholepressure while having complete isolation from the well fluid media bymeasuring the flowing pressure on surface of a gas bubbling at thebottom of a capillary tube in a well. The measurement instrument can belocated potentially thousands of feet from the bottom of a well. Thisisolation makes the bubble tube system suitable for use in wells withcorrosive, acidic, hazardous, liquids at very hot temperatures. It isintrinsically immune to surface foam, pH, conductivity, temperature,turbulence, viscosity, and solids content.

Various aspects of the invention will now be described with reference tothe figures. For the purposes of illustration, components depicted inthe figures are not necessarily drawn to scale. Instead, emphasis isplaced on highlighting the various contributions of the components tothe functionality of various aspects of the invention. A number ofpossible alternative features are introduced during the course of thisdescription. It is to be understood that, according to the knowledge andjudgment of persons skilled in the art, such alternative features may besubstituted in various combinations to arrive at different embodimentsof the present invention.

Overview of the Separator System

One aspect of the present invention is a separator device constructedfor use in a system for separation and recovery of gas trapped in a gaswell by fluid and particulate matter such as fine mud and/or silt. Tofacilitate a discussion of the separator device, the separator systemwill first be discussed in general terms, followed by a more detaileddescription of the features of the device itself.

Turning now to FIG. 1, there is shown a cross-sectional illustration ofone embodiment of a system 100 for recovery of oil and gas trapped in agas well by fluid and particulate matter in accordance with the presentinvention. The system 100 is deployed in the casing 5 of an oil or gaswell and includes a separator device 110 which is deployed below theperforations 7 in the casing 5. The device 110 is formed by a hollowcylindrical body 112 with a cap 114 attached to the open top of the body112. The cap 114 has openings to allow passage of a plurality of linesthat provide specific functions for the separator device 110 asdescribed hereinbelow. The central line in this embodiment of theseparator device 110 is the effluent line 116. On the far left of theeffluent line 116 is the gas line 118 which acts as a dual purpose gascompression and exhaust line. The gas line 118 terminates immediatelybeneath the cap 114. Between the gas line 118 and the effluent line 116is the probe line 120. To the right of the effluent line 116 is thebubble tube line 122.

The features and functions of the four lines 116, 118, 120 and 122 willnow be briefly described. The effluent line 116 carries fluid andsuspended solids out of the well on the compression stroke when theseparator device 110 is operating. The gas line 118 provides pressurizedgas into the separator device 110 during the compression stroke andexhausts gas out of the device 110 during the exhaust stroke. The probeline 120 is an insulated electrical line to provide power to the probes126 and 128 which sense fluid levels in the separator cavity 124 asdescribed in more detail below. The bubble tube line 122 provides ameans for continuously measuring downhole pressure and for cleaning thebottom of the device 110 and the annulus of the well as described inmore detail below.

It is advantageous to make the lines 116, 118, 120 and 122 rigid toavoid kinking and the various problems associated therewith. Therefore,pipes formed of steel or other similarly rigid material or metal alloyare used as the effluent line 116, the gas line 118 and the bubble tubeline 122. In most embodiments, the probe line 120 is a combination ofwires protected by insulation. In one example embodiment, the diameterof the effluent line 116 is about 0.75 inches, the diameter of the gasline 118 is about 0.5 inches and the bubble tube line 122 is about 0.375inches. These dimensions have been found to be appropriate for oneembodiment of a cylindrical separator device with a body 112 having aninner diameter of about 3.188 inches. The skilled person will recognizethat these dimensions are indicative of one embodiment and may bealtered if desired for any reason pertaining to improvement of anyaspect of operation of the separator device 110. Such alternativeembodiments with alternative dimensions are within the scope of thepresent invention.

To retain clarity in FIG. 1, the probe line 120 is shown as beingattached to an upper probe 126 and a lower probe 128 (both shown withblack circles in FIG. 1). Alternative embodiments have a probe line 120which is booted and connected by a tight fitting to the upper and lowerprobes 126 and 128, each mounted separately in the top end of the pumpbody. This arrangement is shown in FIGS. 3A and 3B. Still otherembodiments have probes each supported by two distinct probe lines. Allof these alternative embodiments are within the scope of the invention.The upper and lower probes 126 and 128 are provided to identify twodifferent levels of fluid in the cavity 124 which are reached duringregular cycling of the separator device 110 as described in more detailherein below. Examples of such sensors include but are not limited to,conductivity sensors, tuning fork sensors, optical sensors anddielectric sensors. Any sensor capable of sensing the presence of aliquid may be adapted for use as a probe for use with the presentinvention and such alternatives can be constructed by the skilled personroutinely, without undue experimentation.

In certain embodiments, the probe line 120 is insulated with an abrasiveresistant coating such as polyethylene to prevent electrical shorting.Such coatings are known to the skilled person and can be appliedappropriately without undue experimentation.

In FIG. 1, it is seen that the bubble tube line 122 extends out of thebottom of the separator body 112. The bubble tube line 122 is includedin this embodiment of the system in order to provide a means formeasurement of the reservoir pressure for the purpose of performing ratetransient analysis in accordance with known bubble tube pressuremeasurement methods and also to provide a means for cleaning theseparator device 110 and the annulus of the well by sweeping the bottomof the separator device 110 with high pressure gas. To provide this dualfunction, a bubble tube line valve is provided (as described hereinbelow with reference to FIG. 2) with appropriate connections inaccordance with known methods. Alternative embodiments do not include abubble tube line. In the embodiments that do not include a bubble tubeline, the separator device 110 may be provided with a different meansfor monitoring pressure in the separator device, if desired.

The bottom of the body 112 of the separator device 110 is attached to anadapter 130. The function of the adapter 130 is to provide a means forattachment (for example, by threading) to two nested tubes, an outertube 132 and an inner tube 134 which is nested within the cavity of theouter tube 132. The bubble tube line 122 may extend through the adapter130 and into the space between the nested tubes 132 and 134, or it maybe simply placed adjacent to an opening in the sidewall of the adapter130, which extends via a channel into the space between the innersidewall of the outer tube 132 and the outer sidewall of the inner tube134. This arrangement will be described in more detail hereinbelow withreference to FIG. 7.

Returning now to FIG. 1, it is seen that residing within the cavity ofthe inner tube 134 are an upper valve 136 and a lower valve 138. Thespecific structure and operation of particular embodiments of thesevalves will be discussed in more detail hereinbelow with reference toFIGS. 3A and 3B. For the purposes of this general discussion, it is tobe understood that during the compression stroke of the separator device110 which is initiated when the upper probe 126 senses the fluid levelat its position, pressurized gas enters the cavity 124 via the gas line118. The fluid level in the cavity 124 is forced downward under this gaspressure. This causes the lower valve 138 to close and also causes theupper valve 136 to open, thereby allowing entry and flow of fluid intothe effluent line 116 which is connected to the upper valve 136. On theexhaust stroke, which is initiated by the lower probe 128 sensing thatthe fluid level has dropped to its position, the entry of pressurizedgas into the cavity 124 via the gas line 118 is halted. This allows thefluid level in the cavity 124 to rise again as a result of fluidinfiltration from the reservoir as a result of the removal of fluid fromthe well. Gas remaining in the gas line 118 is vented to thegas-gathering pipeline and reaches pressure equilibrium with thegas-gathering pipeline. With the reduced pressure, valve 136 closes andvalve 138 opens. Fluid enters the bottom of the inner tube 132 and opensthe lower valve 138 to enter the inner tube 134. The hydrostaticpressure of the fluid in the effluent line 116 keeps valve 136 closedand the fluid level gradually increases in the cavity 124 until itreaches the upper probe 126 thereby triggering the next compressionstroke. The separator device 110 will continue to cycle in this manneras long as fluid enters the cavity 124 from the reservoir. The rate offilling of the cavity 124 of the separator device 110 is variable anddepends upon the unique deliverability characteristics of each wellborein a particular reservoir.

The skilled person will recognize from this description that theseparator device 110 operates at a rate which matches the rate ofinfiltration of fluid into the reservoir and thus, the volumes of gasinjected to drive the operation of the separator device 110 are matchedto the requirements of the reservoir.

It is to be understood that the fluid level in the separator device 110and the well will be at its lowest level when the separator device cycleis at the bottom of the compression stroke. Because the fluid level islow at this point, the hydrostatic head pressure of the column of fluidis low and more gas is able to escape from the reservoir via theperforations 7 in the casing 5 of the well. In certain situations, thefluid level will be below the perforations of the well and the reservoirpressure at the perforations will now be at the same pressure as thepressure of the gas gathering line. Therefore, in this situation, gas isproduced uninhibited by a hydrostatic head of fluid and it moves to thesurface gas gathering line via the wellhead 168.

One of the problems addressed by certain aspects of the presentinvention is the removal of fluid containing suspended solids such asfine mud and silt. Such suspended solids will quickly clog the effluentlines of conventional reciprocating or rotating artificial liftequipment. While the separator device of the present invention operateson the general principle of positive gas displacement of fluids, thereis still significant potential for particulate matter such as silt orfine silicate mud particles to enter the gas line 118 on the exhauststroke. Therefore, in certain embodiments, the cavity 124 of theseparator device 110 is provided with a plurality of baffles tointerrupt the upward movement of fluid and particulates in the cavity124 during the exhaust stroke. This interruption of flow causes theparticulates to drop downward and thus, fouling of the gas line 118 isprevented.

The skilled person will recognize that baffles may be attached to orotherwise integrally formed in the inner sidewall of the cavity 124. Amore effective solution is provided as shown in FIG. 1 by constructing aset of baffles 148 a, 148 b and 148 c each having a means for attachmentto one or more of the lines in the cavity 124. This simplifies theconstruction of the body 112. In addition, if the baffles 148 a, 148 band 148 c are substantially equally spaced and supported by each one ofthe three lines that extend down the majority of the length of thecavity 124, the structure of each baffle acts as a centralizer, keepingthe three lines 116, 118 and 120 parallel and generally straight. Thespecific structure of a specific embodiment of set of baffles 248 a, 248b and 248 c is described herein below with reference to FIGS. 4A, 4B and5. The skilled person will recognize that alternative arrangements arepossible wherein the baffles are supported by only one of the threelines which extend down the majority of the length of the cavity 124.Such alternative embodiments are within the scope of the invention.

Returning now to FIG. 1, the features of the system 100 external to theseparator device 110 which are located above the cap 114 will now bedescribed. As noted above, four lines including the effluent line 116,the gas line 118, the probe line 120 and the bubble tube line 122 extendupward through openings in the cap 114. The connectors 152, 154, 156 and158 are located above the cap 114. In certain embodiments, the effluentline 116, the gas line 118, and the bubble tube line 122 are continuouslines extending through the cap 114 to the surface via the wellhead 168and the only line with a connector is the probe line 120.

The area above the cap 114 is provided with a protective pipe 160 whichis connected to the cap 114 by a threading mechanism, for example. Asealing means designated herein as umbilical isolation packer 150 isplaced in the protective pipe 160 above the cap 114 to isolate the upperpart of the system 100 from the separator device 110 because it isadvantageous to restrict fluid from entering this upper part of thesystem 100.

To facilitate assembly of the system 100 in stages, it is advantageousto terminate each of the four lines 116, 118, 120 and 122 extendingabove the cap 114 and to connect each of these lines to upper lines(having the same reference numerals) via connectors 152, 154, 156 and158. The upper lines are then collected and encased in a sheath ofprotective elastomeric material to provide a single umbilical cable 162which extends upwards in the cavity of the protective pipe 160.

It is advantageous to provide the umbilical cable 162 with as muchstrength as possible because it is subjected to significant force ofgravity on its cumulative weight when being deployed into a well by aconventional coiled tubing unit which grips and injects the umbilicalcable into the casing. It has been determined that the structuralstrength of the umbilical cable 162 is improved significantly if thefour lines 116, 118, 120 and 122 contained therein are twisted into arepeating helical pattern prior to covering with the protectivematerial. In one embodiment, the helical pattern for the four lines 116,118, 120 and 122 repeats at intervals ranging between about 8 to about14 inches.

In the embodiment of FIG. 1, the system is provided with a means forwithdrawal of the separator device 110 from the well. The skilled personwill recognize that this means for withdrawal is not required foroperation of the separator device and therefore should be considered anoptional feature. To provide the withdrawal mechanism of thisembodiment, the upper end of the protective pipe 160 is provided with ameans for connection (for example, by threading) to a fishing neck 166which itself is provided with a means for connection to an overshot forconnection to a lifter (not shown). The fishing neck 166 includes a setof slips and packers (not shown) for securely grasping the umbilicalcable 162. This provides a convenient integral mechanism for retrievalof the separator device 110 when it requires maintenance or when gasrecovery operations are complete.

The system 100 also includes a wellhead 168 which allows passage of theumbilical cable 162 while sealing the well. An intermediate section ofthe wellhead 168 is provided with a set of umbilical slips 170 to gripand support the umbilical cable 162 and an umbilical packer 172 abovethe slips to provide further sealing of the well at the wellhead 168. Anadvantageous feature of this particular embodiment is that the fourlines (effluent line 116, gas line 118, probe line 120 and bubble tubeline 122) are separated from the umbilical cable 162 within the body ofthe wellhead 168 and emerge from the wellhead as separately sealeddistinct lines 116, 118, 120 and 122. This feature enhances the securityof the wellhead 168. Detailed views of a specific wellhead embodiment268 are described herein below with reference to FIGS. 9A to 9E.

Returning now to FIG. 1, it is seen that above the wellhead 168, theeffluent line 116 removes fluid from the system 100. The fluid is sentto a tank (not shown in FIG. 1) and the suspended solids are allowed tosettle and then can be separated. In some cases, the suspended solidsare silt or other organic matter which can be used as an agriculturalproduct or fill, for added value. Generally the recovered solid willrequire chemical treatment to be used for agricultural applications.

Referring now to FIG. 2, where the same reference numerals are used toindicate the same features, there is shown a schematic flow diagramindicating how fluid and gas flows through and out of the system 100.The flow of fluids is shown with solid arrows and the flow of gas isshown with dashed line arrows. In this simplified schematic view of thesystem 100, the view of the separator device 110 is simplified relativeto the view of FIG. 1. The effluent line 116, the gas line 118, theprobe line 120, the bubble tube line 122, and the wellhead 168 areshown.

Gas and fluid enters the casing 5 of the well from the perforations 7.The fluid moves downward and enters the separator device 110. The gasmoves upward within the casing annulus and exits the well via aconventional port on the right side of the wellhead 168. This producedgas enters a gas meter 176 and is then directed into the gas gatheringpipeline 174 the gas meter sends a signal to the remote terminal unit(not shown) which determines volumes of gas produced.

The fluid entering the separator device 110 is conveyed out of the wellvia the effluent line 116 during the compression stroke of the separatordevice 110. During proper functioning of the separator device 110 theeffluent line 116 is always filled with fluid and the direction of flowis out of the separator device 110 on the compression stroke with noflow on the exhaust stroke. The effluent line 116 emerges from the welland, in this particular embodiment, is sent to a water tank 178 eitheron site or conveyed to a tank at a remote location.

Gas is removed from the pipeline via a branch conduit 182 and sent to acompressor 184 to pressurize the gas for the compression stroke of theseparator device 110. For efficient functioning of at least some of theembodiments of the system 100 described herein, a pressure range betweenabout 800 to about 1200 psi is used. The pressurized gas follows conduit186 to a 3-way valve 188. On a compression stroke of the separatordevice 110, the 3-way valve 188 will be open between conduit 186 and thegas line 118 and thus the pressurized gas moves down via the gas lineinto the separator device 110 where it pushes fluid into the effluentline 116.

On the exhaust stroke, the flow of pressurized gas into the gas line 118is shut off by the 3-way valve 188 which switches to an exhaust conduit190. This exhaust gas conduit 190 is joined to the gas pipeline 174. Theexhaust stroke is at the same pressure as the gas pipeline 174 and thelength of time for the exhaust cycle depends on the rate of reservoirfluid production into the separator device 110.

The skilled person will recognize that in certain embodiments, the 3-wayvalve 188 may be electrically linked to the probe line 120 so that theprobes which control the timing of the compression and exhaust strokesof the separator device 110 also control the 3-way valve 188. Such anarrangement can be constructed by the skilled person without undueexperimentation. The probe line 120 is connected to an electrical source199 to provide power to the probes which are responsible for switchingbetween the compression and exhaust strokes of the separator device 110.

In addition to providing the source of pressurized gas for driving thecompression stroke of the separator device 110, the compressor 184provides compressed gas to the bubble tube line 122 via conduit 192 whenthe bubble valve 194 is open between conduits 192 and the bubble tubeline 122. The bubble valve 194 is also connected to a source of highpressure cleaning gas 196 via conduit 198. When the bubble tube line 122is connected to conduit 198, high pressure gas is pumped into the bubbletube line 122 and streams outward at the bottom of the separator device110 between the nested tubes formed by the outer tube 132 and the innertube 134 (see FIG. 1) the constriction of flow caused by thisarrangement causes the injected gas to uniformly sweep the bottom of theseparator device 110 to obtain effective cleaning of the annulus definedby the inner sidewall of the casing 5 as well as the bottom valve 138 ofthe separator device 110. A more detailed embodiment incorporating thisfeature is described in more detail herein below with reference to FIG.7.

Operation of the Separator Device

A more detailed description of the operation of the separator device 110will now be described with reference to FIGS. 3A and 3B, where the samereference numerals used in FIGS. 1 and 2 are retained.

Continuing with the same arrow flow scheme of FIG. 2, the flow of gas isshown with dashed arrows and the flow of fluid is shown with solidarrows.

FIG. 3A schematically illustrates the flow of fluid and gas through theseparator device 110 during the compression stroke of the separatordevice 110. Pressurized gas flows into the separator device 110 via thegas line 118 and pushes down on the fluid level in the cavity 124 of theseparator device 110, as indicated by the dashed arrows. The fluid flowsdownward under this pressure. This particular embodiment of theseparator device 110 is provided with two ball valves 136 and 138.Alternative embodiments employ other types of valves. In certainembodiments, the ball valves 136 and 138 include balls 140 and 144formed of plastic such as polyurethane and ball valve seats 142 and 146formed of hard materials such as ceramics.

The fluid flowing downward under pressure during the compression strokeof the separator device 110 causes the lower check ball 144 to drop intothe lower ball seat 146 to close the lower valve 138. The upward flow offluid from the reservoir is thus blocked. The fluid is then forcedupward into the upper valve 136 and the downward motion of the fluidunseats the upper check ball 140 from the upper ball seat 142 to openthe upper valve 136. This allows the fluid to enter the effluent line116. As long as pressurized gas is injected into the gas line 118, fluidwill be forced upward through the effluent line 116 and will exit thetop of the separator device 110. The compression stroke illustrated inFIG. 3A continues until the fluid level reaches the lower probe 128.When the lower probe 128 senses that the fluid level has dropped to orbelow its location, the compression stroke is halted and the exhauststroke begins as illustrated in FIG. 3B.

FIG. 3B schematically illustrates the flow of fluid and gas through theseparator device 110 during the exhaust stroke of the separator device110. The flow of pressurized gas that flows into the separator device110 via the gas line 118 during the compression stroke is now stopped.As a result, the fluid level in the cavity 124 gradually rises (as shownby the solid arrows) in the cavity 124 of the separator device 110 asfluid gradually infiltrates the well from the formation. The fluidenters the cavity 124 via the bottom of the outer tube 132 and thenenters the inner tube 134 where it unseats the lower check ball 144 fromthe lower ball seat 146 in the lower valve 138. This action allows thefluid level to move up into the cavity 124. This upward movement offluid does not have sufficient pressure to unseat the upper check ball140 from the upper ball seat 142 of the upper valve 136. As a result,the bottom entrance to the effluent line 116 remains closed and fluiddoes not move upward in the effluent line 116 during the exhaust stroke.

As noted above, when the fluid level in the well is low, greater volumesof gas can escape from the formation into the well and be captured asproduction gas at the wellhead. The rate of infiltration of fluid willbe dependent upon the characteristics of the formation, and severalhours may pass before the fluid level reaches the upper probe 126 tohalt the exhaust stroke and initiate the compression stroke.

It is to be understood that as the fluid level rises in the cavity 124the baffles 148 a, 148 b and 148 c interrupt this upward flow and theparticulate matter (mud, silt and the like) present in the fluid willtend to drop downward, thereby preventing fouling of the gas line 118.This also enhances the removal of the particulates from the cavity 124via the effluent line 116.

The effect of the fluid level increasing in the cavity 124 is that thepressurized gas remaining in the cavity 124 at the end of thecompression stroke is now displaced out into the lower opening of thegas line. This exhaust gas is sent back to the pipeline as indicated byline 190 via the 3-way valve 188 in FIG. 2.

As described above, one of the functions of the bubble tube line 122 isto perform cleaning operations. Accordingly, in a first mode ofoperation, the bubble tube line 122 is configured to clean the lowervalve 138 of the separator and in a second mode of operation, the bubbletube is configured to clean the area between the casing 5 and theseparator device 110. In the first mode, for cleaning the lower valve138, the cleaning operation is initiated during the exhaust stroke. Inthe second, mode, cleaning of the area between the casing annulus 5 andthe separator device 110 is initiated during the compression stroke.This prevents gas from flowing into the effluent line 116.

Features of Example Embodiments

A number of features of example embodiments of various features of theseparator device and system will now be described. These features may beprovided in various combinations in construction of various alternativeembodiments of the present invention. While the components of the systemand method described using reference numerals in the 100 series in FIGS.1 to 3, more detailed features of the components are described in FIGS.4 to 12 using reference numerals in the 200 series and the 300 series(probes only) while the general features retain their original referencenumerals in the 100 series. Features of a control system are describedwith reference to FIGS. 13A and 13B, which use reference numerals in the500 series.

Centralizer Baffles—As noted above with respect to the baffles 148 a,148 b and 148 c shown in FIGS. 1 and 3, it is advantageous to provide ameans for attachment of the baffles to one or more of the lines thatextend through the cavity 124. In certain preferred embodiments, theselines include the effluent line 116, probe line 120 and the bubble tubeline 122 (there is no opening for the gas line 118 because it terminatesjust below the cap of the separator device and therefore baffles are notattached thereto). Accordingly, there is shown in FIGS. 4A and 4B, oneembodiment of a single leaf-shaped baffle 248 a with a leaf portion 251a a stem portion 253 a and openings in the leaf portion 251 a. Thebaffle 248 a is dimensioned such that its total area is between abouthalf to about two-thirds of the cross sectional area of the cavity,thereby providing a means to block upward movement of particulates suchas silt and sand during the exhaust stroke.

The central opening 255 a is dimensioned to accommodate the effluentline 116, the opening 259 a to the right of the central opening 255 a isdimensioned to accommodate the bubble tube line 122, and the opening 257a to the left of the central opening 255 a is dimensioned to accommodatethe probe line 120, as indicated in FIG. 4B where the probe line 120,the effluent line 116 and the bubble tube line 122 are shown extendingfrom their respective openings 257 a, 255 a and 259 a in the leafportion 251 a of the baffle 248 a. It is to be understood that each ofthe lines 116, 120 and 122 is held in place by the baffle 248 a andthus, a plurality of such baffles will provide the advantage of actingas centralizers to keep the lines straight within the cavity of theseparator device.

Referring now to FIG. 5, there is shown a set of three non-identicalbaffles 248 a, 248 b and 248 c. Each of these baffles differs from theothers in the placement of their respective openings 255 a-c, 257 a-cand 259 a-c. For example, it is seen in baffle 248 a that all of theopenings 255 a, 257 a and 259 a are located in the leaf portion 251 a.In contrast, baffle 248 b has the bubble tube line opening 259 b in thestem portion 253 b and baffle 248 c has the probe line opening 257 b inthe stem portion 253 c.

The different placement of the openings 255 a-c, 257 a-c and 259 a-c ofeach baffle 248 a-c is provided because it is advantageous to rotateeach baffle 248 a, 248 b and 248 c with respect to the longitudinal axisof the separator device body. This arrangement is seen when the bafflesare viewed with respect to the axes of the three lines 116 (effluentline axis 261), 120 (probe line axis 263) and 122 (bubble tube line axis265) in FIG. 5, where it is seen that each of the leaf portions 251 a,251 b and 251 c provides staggered blockage of the cavity of theseparator device in order to slow the upward movement of particulates inthe fluid from rising at the same rate as the fluid level to facilitateremoval of the particulates from the separator device via the effluentline 116 during the compression stroke of the separator device.

It is advantageous in certain embodiments to place the baffles such thatthere is approximately equal spacing between pairs of adjacent baffles.In one preferred embodiment, the separator device body is about 217.25inches long and adjacent pairs of baffles are separated from each otherin the cavity at a distance of about 71 inches with the lowest bafflelocated about 52.75 inches above bottom end of the separator devicebody.

While this preferred embodiment provides a set of baffles 248 a, 248 band 248 c configured to hold three lines in the cavity 124, the skilledperson will appreciate that alternative baffle sets may be providedwhich are configured differently. For example, in alternative separatordevice embodiments which do not include a bubble tube line, the bafflesmay be configured to be supported by only the effluent line 116 or onlythe probe line 120 or by both the effluent line 116 and the probe line120. Furthermore, the baffle set shown in FIG. 5 may be modified toinclude additional or fewer baffles or may be used in the alternativeembodiment when a bubble tube line is not included in the separatordevice. All of these alternative embodiments are within the scope of theinvention.

The skilled person will also appreciate that baffles may also beprovided in shapes other than the leaf shape described in the embodimentof FIGS. 4 and 5. Separator devices constructed according to theprinciples of the present invention and provided with baffle sets havingalternative square, circular or oval shapes are also within the scope ofthe invention.

Adapter for Connection of Nested Tubes and Bubble Tube Line—As describedhereinabove with respect to FIGS. 3A and 3B, in a preferred embodiment,the bottom of the separator device 110 includes nested tubes 132 and 134which are connected to the bottom end of the separator device body 112using a hollow adapter 130. A specific adapter embodiment 230 isillustrated in two perspective views in FIGS. 6A and 6B and showing theconnections to the nested tubes 132 and 134 in FIG. 7. It is seen thatthe adapter 230 includes a narrow portion provided with inner tubethreads 231 for connecting the inner tube 132 and an intermediate widerportion with outer tube threads 233 for connecting the outer tube 134.The adapter 230 is also provided with a recessed outer sidewall 235 atits upper end. This recessed outer sidewall 235 is dimensioned to residewithin the lower end of the cavity 124 of the separator device body 112.This recessed outer sidewall 235 may be provided with threads forconnection to the lower end of the separator device body 112 (if theinner sidewall of the lower end of the body 112 is likewise providedwith appropriate mating threads) or the connection of the adapter 230 tothe body 112 may be made permanent by welding.

The inner sidewall 237 of the adapter 230 is provided with an openingdesignated herein as the bubble tube entrance 239 (see FIG. 6A) whichholds the bubble tube line 122 in place. The bubble tube entrance 239leads to a channel in the inner sidewall 237 of the adapter 230 whichends in an intermediate opening designated herein as the bubble exitport 241. Because the bubble exit port 241 is located at an intermediateposition between the inner tube threads 231 and the outer tube threads233, when the nested tubes 134 and 132 are connected to their respectivethreads 231 and 233, the bubble exit port 241 is located in the spacebetween the inner tube 134 and the outer tube 132.

As indicated by the dashed arrows in FIG. 7, the provision of the bubbleexit port 241 between the nested tubes 132 and 134 provides enhanceduniformity of flow of high pressure gas into the bottom of the separatordevice 110 because the flow of gas from the bubble tube entering thespace between the outer sidewall of the inner tube 134 and the innersidewall of the outer tube 132 becomes dispersed around thecircumference of the bottom of the separator device 110. This isparticularly advantageous for uniform cleaning of the separator device110 and the annulus of the well.

Control Ball Valves—As described hereinabove, the separator deviceincludes a pair of valves which control the movement of fluid during thecompression and exhaust strokes. During the compression stroke, thelower valve is closed and the upper valve is open to force fluid up intothe effluent line and out of the well. During the exhaust stroke, thelower valve is open and the upper valve is closed to allow fluid toinfiltrate into the separator device cavity. In one preferredembodiment, both valves reside within the inner tube of the nested tubesdescribed above. A cross sectional illustration of this arrangement isshown in FIG. 8 which also shows how the bottom end of the separatordevice body 112 is connected to the adapter 230. The probe line 120, theeffluent line 116 and the bubble tube line 122 are shown inside thecavity 124. The outer tube 132 and the inner tube 134 are connected tothe lower end of the adapter 230 with additional sealing provided byo-rings 245 and 247, respectively.

It is further seen in the embodiment of FIG. 8 that the effluent line116 extends through the cavity of the adapter 230 into the cavity of theinner tube 134. The end of the effluent line 116 is attached to theupper valve cap 236 and the upper valve body 249 with an interveningo-ring 243. The upper check ball 240 rests in the curved upper ball seat215 at the bottom of the upper valve body 249. The bottom of the uppervalve is provided with an upper valve bottom cap 211 which has anopening that permits entry of fluid during the exhaust stroke of theseparator device.

The lower valve body 217 is fixed to the bottom end of the inner tube134. The lower valve body 217 includes a curved lower ball seat 213 andthe lower check ball 244 sits in the lower ball seat 213 when the valveis closed during the compression stroke of the separator device. Thelower valve body 217 has a lower valve bottom cap 219 attached thereto,which has an opening that permits entry of fluid into the cavity duringthe exhaust stroke of the separator device.

In certain embodiments, both check balls are constructed of polyethyleneor other material with similar properties and their respective seats areidentically constructed of ceramic material, or other material withsimilar properties.

Wellhead—According to certain aspects of the invention, the separatordevice system includes a wellhead for preservation of well pressure andreinforced support of the lines required for operation of the separatordevice. As described hereinabove, the bubble tube line 122 is optionalin certain embodiments of the separator device. However, in FIGS. 9A to9E which illustrate various views of one embodiment of a wellhead 268which is configured to hold a bubble tube line 122 as well as theeffluent line 116, the gas line 118 and the probe line 120.

FIG. 9A shows a perspective view of a partially constructed wellheadconsisting of a lower wellhead body 269 with a production pipe 271extending therethrough. The production pipe 271 is open to a gaspipeline and provides a passage of produced gas to the gas pipeline (notshown) which leads away from the well. It is also seen in FIG. 9A thatthe umbilical cable 162 extends into the space above the lower wellheadbody 269 and the four lines contained in the umbilical cable 162 areseparated.

FIG. 9B shows a perspective view of the partially constructed wellheadafter installation of an upper wellhead body 273 on top of the lowerwellhead body 269. The four separated lines (116, 118, 120 and 122)extend from the open top of the upper wellhead body 273. Also shown inFIG. 9B is a side valve 275 in the upper wellhead body 273. The purposeof the side valve 275 is to provide a means for bleeding any excesspressure or fluid buildup in the upper well body 273 which could occurin the event of fluid or gas leaks within the cavity of the upperwellhead body 273. The upper wellhead body 273 contains a polyurethaneseal to isolate the umbilical cable 162 from the umbilical slips andallow gas production to flow from the umbilical cable and casing annulusvia the valve installed on the production pipe 271 into the meteringsystem in the wellhead valve box (not shown). The upper wellhead body273 contains the well's flowing and shut in pressure in a closed systemwhen the separator device is filling with reservoir fluid during theexhaust stroke.

FIG. 9C shows a perspective view of the completed wellhead 268.Additional components added in this view are a housing 279 which isprovided with channels to accommodate the upwardly extending lines 116,118, 120 and 122. A top nut 277 is placed over the housing 279 and isthreaded thereto. Each individual line is provided with a sealingelement and a connector for connection to outwardly extending lines forconveyance of electricity, pressurized gas, bubble tube gas andeffluent.

FIG. 9D shows a top view of the wellhead for the purpose of indicating across section along lines L-L of the wellhead. The cross section isshown in FIG. 9E. This cross section shows the umbilical cable 162extending through the wellhead and separating into the effluent line 116and the bubble tube line 122. These lines extend out of the top of thewellhead 268 through respective channels in the housing 279. It is seenthat within the cavity of the upper wellhead body 273 the effluent line116 and the bubble tube line 122 are sheathed in the umbilical cable162, which is supported by a set of umbilical slips 270 and umbilicalpackers 272. The umbilical slips 281 are located within and are retainedby the inner sidewall of the lower wellhead body 271 and are providedwith inner ridges to form a stronger gripping interface with the outersheath of the umbilical cable 162. The umbilical packers 272 residewithin the upper wellhead body 273 and provide an additional sealingfeature to prevent loss of fluid or gas from the wellhead 268 if leaksoccur below the wellhead 268.

In this particular embodiment, lines 116, 118, 120 and 122 are sealedseparately in housing 279 to act as a redundant seal in case of failureof the polyurethane seal between the umbilical cable 162 downhole at thetop of the separator device and the fishing neck fails and allowsfugitive gas to travel up the umbilical cable in the space between thelines 116,118,120 and 122. These lines are roped and twisted during themanufacturing process of umbilical cable 162 and then a polyethylenejacket is applied. Each individual line is sealed because, in someembodiments there is sufficient free space between the lines to allowproduced gas to travel to the surface and be released to theenvironment. Valve 275 on the upper wellhead 273 can be openedperiodically to verify that bottom seals remain intact. Normally thepressure in the upper wellhead body cavity is zero.

In certain embodiments, the wellhead is compatible with injection of a1.625 inch umbilical cable into the well for deployment and operation ofthe separator device system into the well. In certain embodiments thewellhead is rated for 600 ANSI and appropriate for gas wells having asurface pressure up to 1,440 psi.

In certain embodiments, the umbilical packer units 272 are furtherprovided with sealing features to retain a sealed wellhead in the eventof leakage of gas or fluid from fluid or gas lines below the wellhead.

Umbilical Cable—One embodiment of the umbilical cable is shown in FIG.10 in cross section. The outer body of this particular embodiment of theumbilical cable is a flexible sheath formed of high density polyethylenewith an outer diameter of about 1.625 inches. This embodiment of theumbilical cable 262 holds a stainless steel effluent line 216 with anouter diameter of about 0.75 inches, a stainless steel gas line 218 withan outer diameter of about 0.5 inches, a probe line 220 covered withinsulation of cross-linked polyethylene with a polyurethane jacket to anouter diameter of about 0.393 inches, and a stainless steel bubble tubeline 222 with an outer diameter of about 0.375 inches.

To enhance the rigidity of the umbilical cable 262 for protectionagainst the forces of high pressure gas, four filler rods 285 a, 285 b,287 a and 287 b are provided to partially fill the spaces between theeffluent line 216, the gas line 218, the probe line 220 and the bubbletube line 222. In this embodiment, the two large diameter filler rods285 a and 285 b have outer diameters of about 0.24 inches and the twosmaller diameter filler rods 287 a and 287 b have outer diameters of0.18 inches. In this embodiment the filler rods are formed of twistedpolypropylene. The remaining space of the cavity of the umbilical cable262 is occupied by fibrillated polypropylene filler 289. Advantageously,a binder tape 291 is provided between the outer surface of thefibrillated filler 289 and the inner surface of the outer sheath 281.

This embodiment of the umbilical cable is designed to protect thefunctional lines within the cable from the high pressure of gasinfiltration into the annulus of the well from the perforations of thewell and from high pressure gas injected through the bubble tube line222 during a cleaning operation. In addition, significant force isimparted within the separator cavity during the transition from thecompression stroke to the exhaust stroke. The lines and filler rods ofthis embodiment of the umbilical cable 262 are twisted in a helicalpattern along the length of the umbilical cable 262 to enhance therigidity of the cable.

Connectors for the effluent line, the gas line and the bubble tubeline—The inventor of the present invention has recognized that operationof downhole equipment in a typical liquid-loaded gas well increases thechances that such equipment will become stuck in the well from time totime due to the volumes of silt and sand present in the well. Withrespect to certain embodiments of the separator device of the presentinvention, the inventor has also recognized that the presence ofintegrally connected equipment above the separator and extending to thesurface, would complicate fishing operations aimed at removing theseparator from the well if and when it becomes stuck. Therefore, certainembodiments of the invention include provision of the probe line, thegas line, the effluent line and the bubble tube line each in two partswith connections made a location above the cap of the separator andbelow the umbilical cable, as shown in a general manner by connectors152, 154, 156 and 158 of FIG. 1. A means for conveniently disconnectingthese lines above the separator body to allow withdrawal of the linesprior to initiation of fishing operations is also included in someembodiments.

It is readily seen in FIG. 1 that each of the four functional lines 116,118, 120 and 122 emanates from the umbilical cable 162 within theprotective pipe 160 which is covered at its uphole end by a transitionpiece 164. Connectors 152, 154, 156 and 158 are provided to makeconnections with corresponding lines located above the cap 114 of theseparator device 110 when the separator system 100 is deployed in awell. In one particular embodiment, the group of separators is providedwith at least one connector having a weak point which, when disengaged,allows all four of the functional lines extending above the separatordevice to be disengaged from the separator above the cap 114 of theseparator 110. This allows deployment of fishing equipment to retrievethe separator device. (In one embodiment, shown in FIG. 1, the separatordevice 110 is provided with a fishing neck 166 which provides a positionconfigured for connection of fishing equipment for retrieval of theseparator device 110).

In one embodiment, the weak point connection is made at any one or moreof the effluent line, the gas line and the bubble tube line which insome embodiments are each represented by a rigid pipe constructed ofstainless steel or other material with similar properties. In oneembodiment, the probe line is represented by a combination of threewires wrapped in insulation, as indicated for example, in FIG. 10.Embodiments for connection of upper and lower parts of the probe linewill be described in more detail hereinbelow.

One embodiment of a connector system having a weak point and designedfor bridging an upper rigid pipe and a lower rigid pipe is shown inFIGS. 11A to 11D and is illustrated as bridging an upper effluent line116 a and a lower effluent line 116 b. The skilled person will recognizethat the same connector system may also be used to connect upper andlower parts of the gas line and/or the bubble tube line (lines withdifferent diameters will require receptacles with different diameters.The connector system includes an upper receptacle 221 a permanentlyattached by welding, for example, to the upper effluent line 116 a and alower receptacle 221 b similarly attached to the lower effluent line 116b. The connector system further includes a female connector 226configured for installation into the lower receptacle 221 b by threadingtherewithin. Likewise, a male connector 223 is configured forinstallation into the upper receptacle 221 a by threading therewithin.In certain embodiments, the threading system may be provided by aSwagelok threading arrangement.

The lower end of the male connector 223 fits into the wider loweropening of the female connector 226 as best seen in FIGS. 11B and 11C.As shown in FIGS. 11C and 11D, the inner sidewall of the femaleconnector 226 has a recess 225 that receives an adjustable lockingspring 224 installed in the male connector 223 to provide a lockingarrangement of the connection of the upper effluent line 116 a to thelower effluent line 116 b. A pre-determined withdrawal force causingdeformation of the spring by withdrawing the upper effluent line 116 aat a pre-determined sufficient force disengages the locking spring 224from the recess 225 and allows the upper effluent line 116 a to beseparated from the lower effluent line 116 b. In certain embodimentswhere the separator device is deployed at a depth of about one thousandmeters, the locking spring 224 is set to disengage from the femaleconnector 226 when the withdrawal force is about 7,000 pounds. Thisforce limit will vary according to the depth of deployment of theseparator device.

This embodiment also contains a means of sealing the connection. Thesealing means of this embodiment is provided by a pair of o-rings 227 aand 227 b which reside in a pair of corresponding grooves 228 a and 228b formed in the outer sidewall of the male connector 223.

As noted above, the purpose of separating the functional lines above theseparator device is to facilitate their withdrawal prior to conducting afishing operation to remove the separator device from the well. It isadvantageous to make the process of disengagement of the upper linesfrom the lower lines as simple as possible. Therefore, in certainembodiments, the same connector system is used to connect the uppereffluent line, the upper gas line and the upper bubble tube line totheir respective lower lines (providing three separator systems forconnecting upper and lower parts of the effluent line, the gas line andthe bubble tube line). However, it is advantageous to provide only asingle weak point because all three lines are removed simultaneously ata constant rate by a coiled tubing injector which grips and withdrawsthe umbilical cable within which they reside. Therefore, the lockingspring and corresponding recess is omitted from two of the threeconnector systems used. In one such embodiment, only the effluent lineis provided with the locking spring system, as shown in FIGS. 11B to11D. This would avoid the possibility of having multiple weak points setat different disengagement limits. Therefore, in a situation where theupper lines are being removed from the well, as soon as thepredetermined withdrawal force is exerted on all three of the lines (bypulling on the umbilical cable) the locking spring in the connectorsystem of the effluent line will disengage and all three connectorsystems will then be disconnected simultaneously, leaving only theseparator device in the well. In this embodiment and similarembodiments, the receptacle threading systems must be configured towithstand the predetermined pressure, otherwise the male and/or femaleconnectors would become disengaged from the receptacle threading systemsbefore the locking spring mechanism.

Probes—As noted above, the probes are provided to sense the presence offluid levels initiate transitions between compression strokes, wherefluid is forced out of the separator via the effluent line, and theexhaust strokes, where the level of fluid rises in the separator deviceand gas is exhausted via the gas line.

In one embodiment, electrical grounding and ungrounding of the probesinitiates the transitions. Thus, during normal cycling of the separatordevice, when fluid reaches the upper probe, it grounds the probe andinitiates the compression stroke. When fluid passes just below the lowerprobe, this probe is ungrounded and the exhaust stroke is initiated.Like the connectors for the effluent line, the gas line and the bubbletube line described above, it is advantageous to provide a means forconveniently engaging and disengaging the probes from the probe line sothat the upper probe line (the majority of which also resides in theumbilical cable), can be withdrawn at the same time as the other upperlines, as required.

In certain embodiments, the probe line connector system is distinct fromthe gas and fluid line connectors described above. One exampleembodiment of a pair of probes is shown in FIG. 12 with componentsidentified using reference numerals in the 300 series in associationwith general components of a separator device identified using referencenumerals in the 100 series. There is an upper probe 301 and a lowerprobe 311 shown in association with the cap 114 of the separator device.The probes 301 and 311 are similarly constructed but have differentlengths with the lower probe 311 being longer than the upper probe 301as shown. The upper ends of both probes 301 and 311, have conductingpins 302, 312 extending outward from the cap 114. These pins are used tomake plug-in electrical connections with the upper probe line (notshown). Advantageously in this particular embodiment, the connection ofthe pins 302, 312 of the probes 301, 311 to the upper probe lineemanating from the umbilical cable (not shown) is made using aprotective boot covering to protect the connection from moisture. Theprotective boot structure contains a mating receptacle for each of thepins 302, 312 to form the electrical connection with the upper probeline.

One embodiment of the boot structure (not shown) is a Y-shaped boot (notshown) constructed of rubber or other insulating protective materialwhich is then connected to the individual wires emanating from theumbilical cable (not shown). This Y-shaped structure is reversiblyconnectable to the pins 302, 312 in a plug-in arrangement. In certainembodiments, the protective boot is a Y-shaped Kemlon K16 protector boot(Kemlon, Pearland, Tex., USA; www.kemlon.com). Advantageously, thisprobe arrangement is resistant to pressures as high as 20,000 psi. Theprotective boot structure also provides for connection of a ground wireof the probe line to a ground pin 320 which is attached to the cap 114to provide the grounding function required by the probes 301, 311.

In this particular embodiment, the probes 301 and 311 are installedwithin the body of the cap 114 of the separator device by threaded capattachments 305, 315 which allow the upper pins 301, 311 to extendoutward from the cavity 124 of the body 112 of the separator device. Assuch, both probes are conveniently threaded to the cap 114 before thecap 114 is connected to the body 112 of the separator device. Thethreaded cap attachments 305 and 315 are each provided with acorresponding seal 306, 316 such as an o-ring and are each provided withlower hex nut portions to allow up to about 85 foot-pounds of torqueduring tightening of the cap attachments 305 and 315 into the body ofthe cap 114 such that the upper pins 302 and 312 extend upward from theupper surface of the cap 114.

It is seen in FIG. 12 that the lower probe 311 has a total lengthgreater than that of the connector body 304 of the upper probe 301 inorder to place the lower probe near the bottom of the separator devicewhere it defines the lower boundary of fluid level in the separator atthe end of the compression stroke. Lower connector pins 303 and 313 arelocated at the lower termini of the connectors 301 and 311 are exposedfor sending the presence of fluid.

In this particular embodiment, both probes 301 and 311 have rigidcylindrical bodies 304, 314 advantageously constructed of acorrosion-resistant alloy, such as Inconel or other similar material.Advantageously the threaded cap attachments 305 and 315 are formed ofthe same material as the probe bodies 304 and 314.

It is seen in FIG. 12 that the probe body 314 of the lower probe 311 ispermanently attached (by electron beam welding for example) to aprotective tube 317 such as a stainless steel tube, for example. Thistube 317 is shown in cross section to show that the conducting wire 318is held within the tube 317 and makes a connection to the lower pin 313.The interior of the tube 317 is provided with insulation 319. A similararrangement exists in the upper probe 301 but is not shown in crosssection in FIG. 12.

In one embodiment, the upper probe 301 has a total length of about 5.96inches and the lower probe 311 has a total length of about 240 incheswith the majority of its length provided by the protective tube 317 asshown. Additionally, the outer and inner diameters of the protectivetube 317 are about 0.375 inches and about 0.25 inches, respectively.

Control System—Certain embodiments of the invention include a controlsystem. FIGS. 13A and 13B illustrate one embodiment of such a controlsystem. In this illustration, the flow of gas is indicated by a dashedline, the flow of fluid is indicated by a solid line and thetransmission of data is indicated by a dot-dashed line. The wellsiteinstallation 500 a of this particular embodiment includes a gas well 502with a separator device 504 connected to a wellhead 506 and a data andvalve control panel 508 connected thereto. The control panel 508includes a series of valves and sensors that measure pressure andcontrol the flow of gas to and from the separator 504 and measure theflow of fluid produced by the separator 504 during the separationprocess. The control panel 508 also measures the volumes of gas producedby the well 502. Data relating to the measurements described above aremeasured in the control panel 508. The well site installation 500 asends produced gas from the well 502 to the control panel 508 via gasconduit 541 and then to a compressor 603 at the plant 600 via conduit543 a. Data are collected at the control panel 508 and sent to theremote terminal unit 510 via data conduit 549 and then to the masterterminal unit 601 at the plant 600 via conduit 551 a.

The control panel 508 is in data communication with the remote terminalunit 510 which includes a transmitter for sending data to a masterterminal unit 601 at the central plant 600. The master terminal unit 601also has a transmitter for sending command instructions such asinstructions to initiate separator cleaning operations and/or softwareupdates to the remote terminal unit 510 for controlling or reprogrammingthe control panel 508.

One example of a command instruction is a remotely-generated instructionby the operator to over-ride the signal probes in the separator toimmediately generate either a compression stroke or an exhaust stroke.Gas is obtained via delivery line 531 a connected to the wellsiteinstallation 500 a from a compressor 603 at the plant 600 the watervapor is removed from the gas by a dehydrator 607 prior to being routedto the control panel 508 at the separator installation 500 a viarecycled gas delivery line 531 a. When the separator is located at adepth of 1200 feet for example, the requirement for recycled gasrequirement is 1 mscf/d for each 2 bfpd produced from the effluent line(this represents only a small fraction of the produced gas of the gasgathering network from additional wellsite installations 500 a-d withthe majority of the produced gas being sent for gas pipeline sales viaconduit 633). In certain embodiments, there is a pressure sensor at theplant. If the gas recycle delivery line falls below a low pressure setpoint a valve opens and the compressor sends recycled gas back into theline, until the high pressure set point is reached and the deliveryvalve at the plant closes, waiting for the pressure in the system tofall and the cycle repeats itself.

The operator can initiate a cleaning cycle remotely using the bubbletube 504. In this example, the operator reviews production data sentfrom the remote terminal unit 510 to the master terminal unit 601 viaradio 551 a and relayed to the operator via the internet) and notes thatthe production at the well does not meet expectations. Suspecting thatthere is a blockage caused by clumping of particulates in the annulus ofthe well 502, the operator enters the instruction to initiate the manualbubble tube clean out valve stroke. This instruction is transmitted viaradio 553 a to the remote terminal unit 510 and then to the controlpanel 508. The command by the operator is initiated via conduit 557 toswitch the constant flow of bubble tube gas provided by the compressor603 to the separator 504 via conduits 535 and 539 to gas from a highpressure gas source 512. This is done by controlling a two-way valve 514to draw from the high pressure gas source 512 via conduit 537. The highpressure gas is then sent to the bubble tube in the separator 504 viagas conduit 539. This high pressure gas emerges from the bubble tube atthe bottom of the separator 504 and sweeps the annulus of the well 502to remove the blockage.

Data collected at the control panel 508 and sent to the remote terminalunit 510 include, but are not necessarily limited to: downhole pressuremeasured using the bubble tube system, stroke cycles and fluidproduction volumes and rates, as well as gas production volumes andrates. Other sensors and regulators may be incorporated into the controlpanel 508 such as sensors for temperature and fluid densitymeasurements. Such alternative embodiments may be constructed by theskilled person without undue experimentation. In certain embodiments,the operator may access the master terminal unit 601 at a remotelocation from the plant 600 via the internet (as shown in FIG. 13B). Inthis embodiment, the control system is used to control a plurality ofadditional wellsite installations 500 b-d and alerts are provided to theoperator only in the event that data transmitted from a particularseparator installation indicates that its performance has dropped belowa pre-determined threshold. The parameters defining optimal andsuboptimal performance may be adjusted by the operator based on theoperating history of any particular well. The skilled person willrecognize that such parameters may vary significantly as a result offluid loading rates, the volumes of particulates present in the fluidand the gas reserves at any particular wellsite installation. Softwarefor analyzing separator performance is provided with data analytics thatcan be programmed by the skilled person without undue experimentation.

In this embodiment, produced gas from each of the additional wellsiteinstallations 500 b-d is sent to the compressor 603 at the plant 600 forsubsequent dehydration, recycling and sales as shown. Additionally,fluid removed from the loaded wells is sent to the water tank 605.Although not shown to preserve clarity, recycled gas is sent to each ofthe additional wellsite installations 500 b-d to drive the cycling oftheir respective separators and data and commands are transmitted andreceived at remote terminal units installed at each of the additionalwellsite installations 500 b-d.

In certain embodiments, gas produced from the well 502 is measured by aturbine meter and producing pressure by a transducer, the data is sentto the remote terminal unit 510 for digitizing prior to being sent tothe master terminal unit 601. Surface gas pressure is compared to thebubble tube transducer pressure and used to calculate a fluid level.These data sets are also digitized in the remote terminal unit 510 priorto transmission to the master terminal unit 601.

In certain embodiments, the probes of the separator 504 are attached bya signal cable (conduit 547) directly into the remote terminal unit 510.When the separator cavity is full, the probes are grounded and a circuitin the remote terminal unit 510 sends a signal to a solenoid in thecontrol panel 508, which in turn initiates the compression stroke. Theremote terminal unit 510 receives this data, converts it to a fluidproduction volume and sends it to the master terminal unit 601.

The control panel 508 includes a micrometer delivering bubbles of gas tothe bubble tube. The downhole pressure is measured by a pressuretransducer located in the control panel 508 and the pressure data issent to the remote terminal unit 510 and then to the master terminalunit 601 where it is subjected to calculations for rate transientanalysis to assess the performance of the well 502. Additionally, thebubble tube pressure is compared to the casing gas producing pressure tocalculate the fluid level. This data is also processed by the remoteterminal unit 510 and transmitted to the master terminal unit 601.

In certain embodiments, the remote terminal unit 510 uses a radio andantenna to send all data to the master terminal unit 601. The masterterminal unit 601 has software configured to provide an analysis of theperformance of each of the separator installations in the separatornetwork. The software calculates a production decline curve for eachseparator installation and is configured to provide an alert to theoperator if the performance falls below a pre-determined sub-optimallevel. The operator can then interpret the data and decide on actions toimprove performance, such as the bubble tube cleaning operationdescribed above.

As described above, the fluids and gases are conveyed to the plant 600from the separator installations 500 a-d. This significantly reduces thefrequency for pipeline pigging and eliminates a requirement for truckingof fluids to the plant 600.

In some embodiments, the gas recycling line (exemplified by line 531 ain FIGS. 13A and 13B), is a polyethylene tube which is provided with abraided polyester jacket between the tube and a sheathing material toenhance its resistance to the high pressure gas travelling in this line.In certain embodiments, this braided polyester jacket increases thepolyethylene tube's resistance to bursting by a factor of about 10,thereby allowing gas to be carried in the tube at pressures in thevicinity of 1,000 psi. Advantageously, this gas recycling line iscontained in a trench that extends from the plant 600 to the wellsiteinstallation 500 a and the trench also holds line 543 a which carrieseffluent fluid from the wellsite installation 500 a to the water tank605 at the plant 600.

EXAMPLES Example 1 Enhancement of Gas Production Rate in a Fluid-LoadedGas Well

In this example, an existing liquid-loaded gas well of the Milk Riverformation in Alberta was experiencing its final phase of productionusing existing siphon string technology. As indicated in FIG. 14,modelling of the rate of decline of this well using the siphon stringtechnology (solid line) indicated that it would decline to zero byapproximately the year 2030. It was predicted that replacement of thesiphon string technology with a wellsite installation with a separatordevice and related equipment according to one embodiment of theinvention would double the production rate and double the lifetime ofthe well. The siphon string equipment was removed from the well and awellsite installation of the present invention was deployed in itsplace. As indicated in FIG. 14, there was an immediate dramatic increasein the production rate and modelling of the rate of decline of the well(solid line) indicated that production would reach zero sometime afterthe year 2080. Therefore, the original predictions regarding theperformance of the wellsite installation of the invention were generallycorrect.

This example indicates that the system and method of the presentinvention operate as intended and produce an increased rate of gasproduction from a liquid-loaded gas well.

Example 2 Analysis of Data Generated at a Test Wellsite Installation

In this example, analysis of data generated at the same wellsiteinstallation described in Example 1 is described. Data were collectedduring the course of operation of the installation from Oct. 1, 2014 toOct. 31, 2014. A number of parameters were investigated in order toassess the performance of the wellsite installation. Data points wereobtained at 15 minute intervals to investigate volumes of gas produced,volumes of water (and silt) produced and the difference between thebubble tube pressure and the casing pressure to determine the fluidlevel.

FIG. 15A is a time course of volume of gas produced (in MSCF), measuredat 15 minute intervals from Oct. 1, 2014 (20141001) to Oct. 31, 2014(20141031). It is seen that the gas production measured is relativelyconstant between 60 and 80 MSCF with a drop to zero occurring betweenOctober 11 and October 15, due to a system shut-down necessitated bypigging issues. It is seen that when the system was re-started on Oct.15, 2014, the rate of gas production resumed to between 60 and 80 MSCFafter a relatively brief re-equilibration period.

FIG. 15B is a time course of the volume of fluid produced from the well(in Bbl). It can be seen the volume drops at regular intervals whichindicate the transition from a compression stroke to an exhaust stroke.A drop in fluid production is seen between approximately Oct. 11 andOct. 13, 2014 due to the system shut-down described above. It is seenthat when the system was re-started on Oct. 15, 2014, fluid productionresumed.

FIG. 15C shows two time course plots of bubble tube pressure and casingpressure. It is seen that the bubble tube pressure and the casingpressure increased during the shut-down period, as expected.

FIG. 16 is a representation of a user interface displaying dataprocessed by the control system in the form of a control window. It isseen that prominent real-time data displayed include downhole pressure,flow rate per day and casing pressure. The “readings” box includes datapertaining to accumulated gas flow, depth of water in well, number ofpump strokes, volume of produced water and battery voltage. The flow ofgases and fluid is illustrated. In the present view of the userinterface, a compression stroke is underway, as indicated by the flow ofhigh pressure gas (solid line) and by the exit of water (long-dashedline) from the well. Additionally, bubble tube gas (short dashed line)is flowing into the separator device. An alternative view of the userinterface during an exhaust stroke would indicate that exhaust gas(double-dot-dashed line) is moving out of the well and that water is notmoving from the well.

This example illustrates some of the capabilities of the control systemin providing useful data to an operator regarding performance of thewellsite installation in producing gas and removing fluid from aliquid-loaded gas well. Such data provide an operator with the abilityto quickly assess and address any production issues that may ariseduring operation of the wellsite installation.

Equivalents and Scope

Other than described herein, or unless otherwise expressly specified,all of the numerical ranges, amounts, values and percentages, such asthose for amounts of materials, elemental contents, times andtemperatures, ratios of amounts, and others, in the following portion ofthe specification and attached claims may be read as if prefaced by theword “about” even though the term “about” may not expressly appear withthe value, amount, or range. Accordingly, unless indicated to thecontrary, the numerical parameters set forth in the followingspecification and attached claims are approximations that may varydepending upon the desired properties sought to be obtained by thepresent invention. At the very least, and not as an attempt to limit theapplication of the doctrine of equivalents to the scope of the claims,each numerical parameter should at least be construed in light of thenumber of reported significant digits and by applying ordinary roundingtechniques.

Notwithstanding that the numerical ranges and parameters setting forththe broad scope of the invention are approximations, the numericalvalues set forth in the specific examples are reported as precisely aspossible. Any numerical value, however, inherently contains errornecessarily resulting from the standard deviation found in itsunderlying respective testing measurements. Furthermore, when numericalranges are set forth herein, these ranges are inclusive of the recitedrange end points (i.e., end points may be used).

Also, it should be understood that any numerical range recited herein isintended to include all sub-ranges subsumed therein. For example, arange of “1 to 10” is intended to include all sub-ranges between (andincluding) the recited minimum value of 1 and the recited maximum valueof 10, that is, having a minimum value equal to or greater than 1 and amaximum value of equal to or less than 10. The terms “one,” “a,” or “an”as used herein are intended to include “at least one” or “one or more,”unless otherwise indicated.

Any patent, publication, internet site, or other disclosure material, inwhole or in part, that is said to be incorporated by reference herein isincorporated herein only to the extent that the incorporated materialdoes not conflict with existing definitions, statements, or otherdisclosure material set forth in this disclosure. As such, and to theextent necessary, the disclosure as explicitly set forth hereinsupersedes any conflicting material incorporated herein by reference.Any material, or portion thereof, that is said to be incorporated byreference herein, but which conflicts with existing definitions,statements, or other disclosure material set forth herein will only beincorporated to the extent that no conflict arises between thatincorporated material and the existing disclosure material.

Unless otherwise defined, all technical and scientific terms used hereinhave the same meaning as commonly understood by one of ordinary skill inthe art to which this invention belongs. Although methods and materialssimilar or equivalent to those described herein can be used in thepractice or testing of the present invention, suitable methods andmaterials are described below.

While this invention has been particularly shown and described withreferences to embodiments thereof, it will be understood by thoseskilled in the art that various changes in form and details may be madetherein without departing from the scope of the invention encompassed bythe appended claims.

1. A system for recovery of gas trapped by fluid and particulate matterin a gas or oil well, the system comprising: a) a device comprising abody defining a cavity with a cap at its upper end and an opening forentry of fluid at its bottom end, the device including a lower valve forcontrolling flow of fluid into the cavity and an upper valve forcontrolling flow of the fluid and suspended solids out of the cavity,the cap having a plurality of lines passing therethrough and into thecavity, the plurality of lines comprising: i) a gas line for providing astream of pressurized gas to push downward on fluid in the cavity in acompression stroke which closes the lower valve and opens the uppervalve, the gas line further used to exhaust contained gas from thecavity during an exhaust stroke when infiltration of fluid into thecavity raises the fluid level in the cavity; ii) an effluent line forallowing exit of the fluid and suspended solids during the compressionstroke; and iii) a probe line for providing electrical power to a pairof probes for initiating and halting entry of the stream of pressurizedgas into the cavity; and b) a wellhead for sealing the well; wherein theplurality of lines extend out from the wellhead, wherein the probe lineis connected to a source of electricity, the gas line is connected to asource of pressurized gas and the effluent line is connected to a fluidstorage unit.
 2. The system of claim 1, wherein the plurality of linesis covered by a single protective covering forming an umbilical cableabove the cap.
 3. The system of claim 1, wherein the device furthercomprises a bubble tube line for determining pressure in the device. 4.The system of claim 3, wherein the bubble tube line is configured to beswitched to a cleaning line for injection of a second stream ofpressurized gas into the device.
 5. The system of claim 3, furthercomprising an adapter attached to the bottom end of the body, theadapter configured for attachment of a pair of nested tubes including aninner tube and an outer tube, the adapter having an opening leading to achannel in the adapter's inner sidewall, wherein the bottom end of thebubble tube is placed at the opening to transmit gas from the bubbletube into a space between an inner sidewall of the outer tube and anouter sidewall of the inner tube.
 6. The system of claim 1, wherein thewellhead includes a set of slips for gripping the umbilical cable tosupport the device in the well.
 7. The system of claim 1, wherein thewellhead is sealed from the well to prevent loss of gas or fluid as aresult of potential leakage of the effluent line or the gas line.
 8. Thesystem of claim 1, wherein the device includes an upper tube connectedto the cap, the upper tube connected to a fishing unit for attachment ofa lifter for withdrawal of the device from the well.
 9. The system ofclaim 8, wherein the fishing unit comprises a fishing neck attached to atop portion of the upper tube and an overshot tube connected to thefishing neck, the overshot tube having a restricted diameter portion forattachment of the lifter.
 10. The system of claim 1, wherein each one ofthe plurality of lines is separated from the protective covering withinthe wellhead and extends from the top of the wellhead as a separateline.
 11. The system of claim 10, wherein each of the separate lines iseach sealed at its respective opening at the top of the wellhead. 12.The system of claim 1, wherein the wellhead includes a production pipeconnected to a gas pipeline and the gas line is connected via athree-way valve to the gas pipeline and a compressor, the three-wayvalve for switching between input of compressed gas into the gas linefor the compression stroke and exhaust of gas back into the pipelineduring the exhaust stroke.
 13. The system of claim 1, wherein each oneof the plurality of lines is formed by an upper line and a lower lineconnected at connection points located above the cap, the connectionpoints permitting disconnection of each of the upper lines from theircorresponding lower lines and withdrawing each of the upper lines fromthe well while the lower lines remain associated with the separatordevice in the well.
 14. The system of claim 13, wherein at least one ofthe connection points represents a weak point with respect todisconnection of all of the upper lines from their corresponding lowerlines.
 15. The system of claim 14, wherein the weak point comprises aconnector with a locking spring mechanism having a variable locking setpoint which, when exceeded allows breakage of the weak point to allowthe upper lines to be withdrawn from the well.
 16. The system of claim1, wherein each of the pair of probes is supported within the cavity bya connection to the cap.
 17. The system of claim 16, wherein theconnection to the cap is made by threaded cap attachments configured tobe threaded into the body of the cap with electrically conductingconnector pins extending therethrough for forming a connection of theupper probe line with the pair of probes.
 18. A method for removingfluid and suspended solids from a gas or oil well to promote productionof gas from the well, the method comprising: a) installing a systemaccording to claim 2 in the well; b) injecting the stream of pressurizedgas into the well in the compression stroke to displace liquid into theeffluent line leading out of the well until the level of the fluid andsuspended solids in the well reaches a lower limit indicated by thelower probe; c) halting the pumping of the gas and allowing the liquidto infiltrate into the well in an exhaust stroke until the level of thefluid and suspended solids reaches an upper limit indicated by the upperprobe; and d) repeating steps b) and c) in sequence.
 19. The method ofclaim 18, further comprising collecting data indicating bottom holepressure, fluid production volumes and gas production volumes to assessthe performance of the well.
 20. The method of claim 18, furthercomprising conducting rate transient analysis from the data, the ratetransient analysis providing a means for modelling a rate of gasproduction decline in the well.
 21. The method of claim 18, wherein thestep a) is performed by conveying the device into the well using acoiled tubing unit, wherein the coiled tubing unit grips and drives theumbilical cable as the umbilical cable is conveyed into the well.
 22. Awellsite installation for controlling production of gas from a gas oroil well, the wellsite installation comprising: a) a system forproducing gas from a well in a process using pressurized gas; b) acontrol panel for controlling and measuring: i) flow of produced gas outof the system; ii) flow of the stream of pressurized gas into thesystem; and iii) flow of the fluid and suspended solids out of thesystem; and c) a remote terminal unit for collection of data obtained atthe control panel.
 23. A gas collection network comprising a plant forreceiving and compressing gas produced from a plurality of wellsiteinstallations according to claim 22, the plant including a compressorfor compressing the produced gas transferred from the wellsiteinstallations and a water tank for storing the fluid and suspendedsolids transferred from the wellsite installations.
 24. The gascollection network of claim 23, wherein the plant further comprises amaster terminal unit for analysis of the data collected at the controlpanel.
 25. The gas collection network of claim 23, further comprising adehydrator located at the plant to remove water vapor from the producedgas.
 26. The gas collection network of claim 24, further comprising amaster terminal unit in data and control communication with the remoteterminal unit, the master terminal unit having a user interfacedisplaying data from the control panel including downhole pressure,casing pressure and flow rate.
 27. The gas collection network of claim23, further comprising a fluid line to transmit the fluid and suspendedsolids to the plant for storage.
 28. The gas collection network of claim25, further comprising a gas recycling line to transmit gas from thedehydrator at the plant to the wellsite installation as the source ofthe stream of pressurized gas for the system.
 29. The gas collectionnetwork of claim 22, wherein the system comprises: a) a devicecomprising a body defining a cavity with a cap at its upper end and anopening for entry of fluid at its bottom end, the device including alower valve for controlling flow of fluid into the cavity and an uppervalve for controlling flow of the fluid and suspended solids out of thecavity, the cap having a plurality of lines passing therethrough andinto the cavity, the plurality of lines comprising: i) a gas line forproviding a stream of pressurized gas to push downward on fluid in thecavity in a compression stroke which closes the lower valve and opensthe upper valve, the gas line further used to exhaust contained gas fromthe cavity during an exhaust stroke when infiltration of fluid into thecavity raises the fluid level in the cavity; ii) an effluent line forallowing exit of the fluid and suspended solids during the compressionstroke; and iii) a probe line for providing electrical power to a pairof probes for initiating and halting entry of the stream of pressurizedgas into the cavity; and a wellhead for sealing the well; wherein theplurality of lines extend out from the wellhead, wherein the probe lineis connected to a source of electricity, the gas line is connected to asource of pressurized gas and the effluent line is connected to a fluidstorage unit.